CN203852937U - Filtering material for high-temperature exhaust gas bag type dust removal system - Google Patents

Filtering material for high-temperature exhaust gas bag type dust removal system Download PDF

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Publication number
CN203852937U
CN203852937U CN201320889290.0U CN201320889290U CN203852937U CN 203852937 U CN203852937 U CN 203852937U CN 201320889290 U CN201320889290 U CN 201320889290U CN 203852937 U CN203852937 U CN 203852937U
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China
Prior art keywords
layer
base cloth
cloth layer
dust removal
filtrate
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Expired - Lifetime
Application number
CN201320889290.0U
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Chinese (zh)
Inventor
刘仁越
徐振宁
田厚忠
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SUZHOU SINOMA CONSTRUCTION CO Ltd
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SUZHOU SINOMA CONSTRUCTION CO Ltd
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Priority to CN201320889290.0U priority Critical patent/CN203852937U/en
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Publication of CN203852937U publication Critical patent/CN203852937U/en
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Abstract

The utility model discloses a filtering material for a high-temperature exhaust gas bag type dust removal system. The filtering material adopts a two-layer structure; one layer is a base cloth layer, and the other layer is a dust removal surface layer covering the base cloth layer; the base cloth layer is made of at least one of glass fibers and chemical fiber machine woven cloth; the dust removal surface layer is made of at least one of the glass fibers and chemical fibers. By the adoption of the two-layer structure, under a condition of guaranteeing the dust removal effect, the filtering material production cost and the later dust removal running cost are effectively lowered, and the use rate of the surface fiber layer of the filtering material is improved.

Description

High-temperature flue gas bag-type dust removing system filtrate
Technical field
The utility model belongs to chemical field, relates to specifically a kind of filtrate, relates in particular to a kind of high-temperature flue gas bag-type dust removing system filtrate.
Background technology
The industries such as cement, metallurgy, electric power give off a large amount of industrial dust in process of production, have a strong impact on living environment and sustainable development, and national requirements for environmental protection is strictly administered it.
In dedusting industry, the electrostatic precipitator concentration of emission of current domestic employing is 100mg/Nm3, and existing standard is 20~30mg/Nm3, cannot meet environmental requirement; Sack cleaner is the most effective means of industrial dust of administering, China Power federation to power industry explicitly call for 2015 the year end all electric power enterprises must adopt bag filter to gather dust, filtering material is the core of bag-type dusting.
The non-coated filter material dust removal mechanism of pocket type is in-depth filtration, mainly relies on the muffin forming after fiber capturing dust to realize the filtration to dust.In use, dust seldom can pass through the fibrous filter layer on top layer, causes the fibrage service efficiency of filtrate inner side lower, causes waste, has increased the production cost of filtrate.
Summary of the invention
In order to overcome above-mentioned defect, the utility model provides a kind of high-temperature flue gas bag-type dust removing system filtrate, in the situation that guaranteeing dust removing effects, effectively reduces filtrate production cost and later stage dedusting operating cost, has improved the utilization rate of filtrate surface fibre layer.
The utility model for the technical scheme that solves its technical problem and adopt is: a kind of high-temperature flue gas bag-type dust removing system filtrate, described filtrate is double-layer structure, wherein one deck is base cloth layer, another layer is for being covered in the dedusting surface layer on this base cloth layer, described base cloth layer is at least glass fibre and chemical fibre woven fabric, and one of them is made, and described dedusting surface layer is at least glass fibre and chemical fibre, and one of them is made.
As further improvement of the utility model, between described dedusting surface layer and base cloth layer, by needling process, be composited.
As further improvement of the utility model, the warp-wise density of described base cloth layer is: 5~20/cm, latitudinal density is: 5~20/cm.
As further improvement of the utility model, the warp-wise brute force >=900N/50mm of described base cloth layer; Broadwise brute force >=450N/50mm.
The beneficial effects of the utility model are: this filtrate adopts double-layer structure, in the situation that guaranteeing dust removing effects, effectively reduce filtrate production cost and later stage dedusting operating cost, have improved the utilization rate of filtrate surface fibre layer.Also compare and have the following advantages with existing filtrate simultaneously:
(1) change the three-decker of ordinary filter, the fibrage that inner side utilization rate is extremely low has been removed, slightly increased dedusting layer thickness simultaneously, when having reduced production cost, ensured the filter efficiency of filtrate;
(2) three-decker is reduced to double-decker, has reduced the intensity of acupuncture, has reduced the damage of needling process to base cloth, has promoted the mechanical property of filtrate;
(3) three-decker is reduced to double-decker, has reduced the filtration resistance of filtrate, has reduced the operating cost of filtrate dedusting.
Accompanying drawing explanation
Fig. 1 is the utility model structural representation.
The specific embodiment
Below with reference to drawings and Examples, the utility model is described in further detail.
As Fig. 1, a kind of high-temperature flue gas bag-type dust removing system filtrate providing for the utility model, for double-decker, the base cloth layer 1 consisting of glass and/or chemical fibre woven fabric comprising one deck, arranges the dedusting surface layer 2 that one deck consists of glass and/or chemical fibre on the upper surface of described base cloth layer 1.
The warp-wise density T of described base cloth layer: 5~20/cm; Latitudinal density W:5~20 piece/cm.
Powerful T >=the 900N/50mm of warp-wise of described base cloth layer; Powerful W >=the 450N/50mm of broadwise.
Between described dedusting surface layer 2 and base cloth layer 1, pass through needling process composite consolidation.
Described filtrate is selected Zhongcai Sci. & Tech. Co., Ltd's patent " a kind of acupuncture surface conditioning agent and impregnation technology thereof " (number of patent application: 200510037950.2) it is carried out to dip finishing.
Below a kind of high-temperature flue gas bag-type dust removing system described in the utility model is given an example by the preparation method of filtrate:
Embodiment 1:
A high-temperature flue gas bag-type dust removing system filtrate, the upper surface of the base cloth layer 1 forming at aramid fiber woven fabric, by needling process, on base cloth layer 1 surface, forming one deck aramid fiber layer is dedusting surface layer 2, and makes it and base cloth layer 1 composite consolidation.
Described base cloth layer radial fragmentation is powerful: T >=900N/50mm; Broadwise ultimate strength W >=450N/50mm.
Described base cloth layer warp-wise density T: 15/cm; Latitudinal density W:15 root/cm.
Described base cloth layer grammes per square metre: 200 ± 5%g/m 2.
Described filtrate is selected Zhongcai Sci. & Tech. Co., Ltd's patent " a kind of acupuncture surface conditioning agent and impregnation technology thereof " (number of patent application: 200510037950.2) it is carried out to dip finishing.
Prepared media performance test result is as shown in table 1.
Table 1 media performance result
Embodiment 2:
A high-temperature flue gas bag-type dust removing system filtrate, the upper surface of the base cloth layer 1 forming at glass fiber weaving cloth, by needling process, on base cloth layer 1 surface, forming layer of glass layer is dedusting surface layer 2, and makes it and base cloth layer 1 composite consolidation.
Described base cloth layer radial fragmentation is powerful: T >=1400N/50mm; Broadwise fracture strength W >=1400N/50mm.
Described base cloth layer warp-wise density: T:8 root/cm; Latitudinal density W:8 root/cm.
Described base cloth layer grammes per square metre: 600 ± 5%g/m 2.
Described filtrate is selected Zhongcai Sci. & Tech. Co., Ltd's patent " a kind of acupuncture surface conditioning agent and impregnation technology thereof " (number of patent application: 200510037950.2) it is carried out to dip finishing.
Prepared media performance test result is as shown in table 2.
Table 2 media performance result
Embodiment 3:
A high-temperature flue gas bag-type dust removing system filtrate, at the weave cotton cloth upper surface of the base cloth layer 1 that forms of PTFE fibre machine, by needling process, on base cloth layer 1 surface, forming one deck PTFE fibrage is dedusting surface layer 2, and makes it and base cloth layer 1 composite consolidation.
Described base cloth layer radial fragmentation is powerful: T >=1000N/50mm; Broadwise ultimate strength W >=650N/50mm.
Described base cloth layer warp-wise density: T:10 root/cm; Latitudinal density W:10 root/cm.
Described base cloth layer grammes per square metre: 140 ± 5%g/m2.
Described filtrate is selected Zhongcai Sci. & Tech. Co., Ltd's patent " a kind of acupuncture surface conditioning agent and impregnation technology thereof " (number of patent application: 200510037950.2) it is carried out to dip finishing.
Prepared media performance test result is as shown in table 3.
Table 3 media performance result
Embodiment 4:
A high-temperature flue gas bag-type dust removing system filtrate, at the weave cotton cloth upper surface of the base cloth layer 1 that forms of acrylic fibre machine, by needling process, on base cloth layer 1 surface, forming one deck acrylic fibrage is dedusting surface layer 2, and makes it and base cloth layer 1 composite consolidation.
Described base cloth layer radial fragmentation is powerful: T >=900N/50mm; Broadwise ultimate strength W >=450N/50mm.
Described base cloth layer warp-wise density: T:10 root/cm; Latitudinal density W:10 root/cm.
Described base cloth layer grammes per square metre: 180 ± 5%g/m2.
Described filtrate is selected Zhongcai Sci. & Tech. Co., Ltd's patent " a kind of acupuncture surface conditioning agent and impregnation technology thereof " (number of patent application: 200510037950.2) it is carried out to dip finishing.
Prepared media performance test result is as shown in table 4.
Table 4 media performance result
Embodiment 5:
A kind of high-temperature flue gas bag-type dust removing system filtrate, the upper surface of the base cloth layer 1 forming at aramid fiber woven fabric, the mixed fiber layer that forms one deck aramid fiber and glass fibre on base cloth layer 1 surface by needling process is dedusting surface layer 2, and makes it and base cloth layer 1 composite consolidation.
Described base cloth layer radial fragmentation is powerful: T >=900N/50mm; Broadwise ultimate strength W >=450N/50mm.
Described base cloth layer warp-wise density: T:15 root/cm; Latitudinal density W:15 root/cm.
Described base cloth layer grammes per square metre: 200 ± 5%g/m2.
The aramid fiber that described aramid fiber and glass composite fibre comprise 20 weight portions and the glass fibre of 80 weight portions, described weight portion is by the aramid fiber in described composite fibre and glass fibre totally 100 listed as parts by weight.
Described filtrate is selected Zhongcai Sci. & Tech. Co., Ltd's patent " a kind of acupuncture surface conditioning agent and impregnation technology thereof " (number of patent application: 200510037950.2) it is carried out to dip finishing.
Prepared media performance test result is as shown in table 5.
Table 5 media performance result

Claims (1)

1. a high-temperature flue gas bag-type dust removing system filtrate, it is characterized in that: described filtrate is double-layer structure, wherein one deck is base cloth layer (1), another layer is for being covered in the dedusting surface layer (2) on this base cloth layer, described base cloth layer is that glass fibre is made, and described dedusting surface layer is at least glass fibre and chemical fibre, and one of them is made; Between described dedusting surface layer and base cloth layer, by needling process, be composited; The warp-wise density of described base cloth layer is: 5~20/cm, latitudinal density is: 5~20/cm; Warp-wise brute force >=the 900N/50mm of described base cloth layer; Broadwise brute force >=450N/50mm.
CN201320889290.0U 2013-12-31 2013-12-31 Filtering material for high-temperature exhaust gas bag type dust removal system Expired - Lifetime CN203852937U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201320889290.0U CN203852937U (en) 2013-12-31 2013-12-31 Filtering material for high-temperature exhaust gas bag type dust removal system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201320889290.0U CN203852937U (en) 2013-12-31 2013-12-31 Filtering material for high-temperature exhaust gas bag type dust removal system

Publications (1)

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CN203852937U true CN203852937U (en) 2014-10-01

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105709503A (en) * 2014-12-05 2016-06-29 东丽纤维研究所(中国)有限公司 Base cloth with high gram weight and filter felt made of same

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105709503A (en) * 2014-12-05 2016-06-29 东丽纤维研究所(中国)有限公司 Base cloth with high gram weight and filter felt made of same

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Granted publication date: 20141001